NF Plant
|
|||||||||||
Mass
Balance
|
|||||||||||
(NF,
Acid whey)
|
|||||||||||
NF of
Acid Whey
|
Unit
|
NF Feed
|
NF
Retentate
|
NF
Permeate
|
|||||||
Capacity
|
kg/h
|
59400
|
40432.986
|
18967.01
|
|||||||
True
Protein
|
%
|
0.4
|
1.65
|
0
|
|||||||
NPN
|
%
|
0.15
|
0.42
|
0.06
|
|||||||
Lactose
|
%
|
3.63
|
0.06
|
11.23
|
|||||||
Acid
|
%
|
0.15
|
0.07
|
0.32
|
|||||||
Ash
|
%
|
0.83
|
0.4
|
1.75
|
|||||||
Fat
|
%
|
0.04
|
0
|
0.13
|
|||||||
NF
Plant Configuration
|
|||||||||||
Membrance
: Filmtec NF
|
|||||||||||
Module
: Spiral Wound, type 3840
|
|||||||||||
|
|
|
|
|
|
||||||
Loop
|
Spacer
|
No. of
Modules
|
Membrane
Element pr. Module
|
Area
(m2)
|
Installed
Effect
|
||||||
1
|
30
|
17
|
5
|
629
|
22KW
|
||||||
2
|
30
|
15
|
5
|
555
|
18.5KW
|
||||||
3
|
30
|
12
|
5
|
444
|
18.5KW
|
||||||
4
|
30
|
13
|
4
|
385
|
18.5KW
|
||||||
|
|
|
Total
|
2013
|
77.5KW
|
||||||
|
|
|
|
|
|
||||||
|
High
Pressure Feed Pump - 1
|
|
|
|
37.0KW
|
||||||
|
High
Pressure Feed Pump - 2
|
|
|
|
37.0KW
|
||||||
|
Total
Effect Installed
|
|
|
|
151.5KW
|
||||||
SC =
Pump must be equipped with a frequency converter.
|
|||||||||||
Consumption
Data
|
|||||||||||
(Membrane
Plant Exclusive of Pre and After Treatment)
|
|||||||||||
Power
Consumption
|
Effect
of Motor (kW)
|
Operating
Hours/day
|
Total /
day (kWH)
|
||||||||
Production
|
156
|
18
|
2808
|
||||||||
CIP
|
93
|
4
|
372
|
||||||||
|
|
Total
|
3180
|
||||||||
|
|
|
|
||||||||
Cooling
Consumption
|
Max.
Capacity (KW)
|
Operating
Hours/day
|
Tatal
/day (kWh)
|
||||||||
Producetion
|
0
|
18
|
|
||||||||
CIP
|
84
|
4
|
176
|
||||||||
|
|
|
176
|
||||||||
Please
note:
|
|||||||||||
Required
for Cooling : Chilled Water at Max. 1 - 2°C
|
|||||||||||
No
Cooling During Production
|
|||||||||||
Cooling
Needed for Approx. 125 min/day
|
|||||||||||
Heating
Consumption
|
Max.
Capacity (KW)
|
Consumption
per day (kWh)
|
|||||||||
CIP
|
715
|
477
|
|||||||||
Note:
|
|||||||||||
The
heating capacity is based on flushing with cold water, the enclosed proposal
for CIP, and on a heating time of 10
minutes per CIP sequence.
|
|||||||||||
Water
Consumption
|
Max.
Capacity
|
Consumption
per day
|
|||||||||
CIP
|
104
m3/h
|
104 m3
|
|||||||||
Water Quality
Specifications
|
|
|
|||||||||
Iron
(Fe) :
|
<
0.05 mg/l
|
|
|||||||||
Manganese
(Mn) :
|
<0.02
mg/l
|
|
|||||||||
Aluminium
(Al) :
|
<0.05
mg/l
|
|
|||||||||
Silica
(SiO2) :
|
<20
mg/l
|
|
|||||||||
Hypochlorite
(Cl2/HOCl):
|
0 mg/l
|
|
|||||||||
German
Hardness :
|
<20°dH
|
|
|||||||||
Conductivity:
|
> 5micronS/cm
|
|
|||||||||
Foulding
Index :
|
<3
SDI
|
|
|||||||||
Turbidity:
|
<1
NTU
|
|
|||||||||
Total
Count at 22°C
|
<1000/ml
|
|
|||||||||
Total
Count at 37°C
|
<10/ml
|
|
|||||||||
Coliforms
per 100ml :
|
<10
|
|
|||||||||
|
|
|
|||||||||
Cleaning
Agent
|
Kg/day
|
|
|||||||||
Ultrasil
67
|
6.4
|
|
|||||||||
Ultrasil
69
|
17.1
|
|
|||||||||
Ultrasil
75
|
6.4
|
|
|||||||||
Ultrasil
110
|
38.5
|
|
|||||||||
Membrance
|
|||||||||||
Type of
Membrane :
|
Filmtec
NF
|
||||||||||
Area
Installed
|
2124 m2
(287 membrane Elements)
|
||||||||||
Suggested
Cleaning Procedure
|
|||||||||||
Type of
Plant
|
NF
Plant
|
||||||||||
Type of
Membrance
|
SW-PE
|
||||||||||
Type of
Feed Product
|
Acid
Whey
|
||||||||||
Operating
temp.
|
10 -
13°C
|
||||||||||
Step
|
Duration
(minutes)
|
Cleaning
Agent
|
Strength
(%)
|
Temp.
(°C)
|
|||||||
Flushing
|
5 - 10
|
Water /
RO permeate
|
|
Cold
|
|||||||
Enzyme
|
35
|
P3
-Ultrasil 69
|
0.8
|
50
|
|||||||
|
|
P3 -
Ultrasil 67
|
0.3
|
|
|||||||
Flushing
|
5 - 10
|
Water /
RO permeate
|
|
Cold
|
|||||||
Acid
|
30
|
P3 -
Ultrasil 75
|
0.3
|
50
|
|||||||
Flushing
|
5 - 10
|
Water /
RO permeate
|
|
Cold
|
|||||||
Alkali
|
30
|
P3 -
Ultrasil 110
|
0.8
|
50
|
|||||||
Flushing
|
5 - 10
|
Water
|
|
Cold
|
|||||||
|
|
|
|
|
|||||||
NF of
Acid Whey
|
NF Feed
|
NF
Retentate
|
NF Permeate
|
|
|||||||
True
Protein %
|
0.4
|
1.65
|
0
|
|
|||||||
NPN %
|
0.15
|
0.42
|
0.06
|
|
|||||||
Lactose
%
|
3.62
|
14.66
|
0.08
|
|
|||||||
Acid %
|
0.15
|
0.53
|
0.03
|
|
|||||||
Ash %
|
0.83
|
2.57
|
0.27
|
|
|||||||
Fat %
|
0.04
|
0.16
|
0
|
|
|||||||
Total
Solids %
|
5.19
|
19.98
|
0.45
|
|
|||||||
Capacity
Kg/hr
|
58,000
|
14,085
|
43,915
|
|
|||||||
Running
Hours Between CIP
|
20
|
20
|
20
|
|
|||||||
Capacity
per day/kr
|
1,60,000
|
281700
|
878300
|
|
|||||||
UF of
Acid NF Retentate (35% WPC)
|
UF Feed
|
UF
Retentate
|
UF
Permeate
|
Powder
with 3.5% moisture
|
|||||||
True
Protein %
|
1.65
|
10
|
0.04
|
|
|||||||
NPN%
|
0.42
|
0.74
|
0.36
|
|
|||||||
Lactose
%
|
14.66
|
14.23
|
14.74
|
|
|||||||
Acid %
|
0.53
|
0.53
|
0.53
|
|
|||||||
Ash %
|
2.57
|
2.96
|
2.5
|
|
|||||||
Fat%
|
0.16
|
0.97
|
0.01
|
|
|||||||
|
|
|
|
|
|||||||
Total
solids%
|
19.98
|
29.43
|
18.17
|
96.5
|
|||||||
Protein
/ Total Solids
|
|
36.5
|
|
|
|||||||
Ash /
Powder
|
|
|
|
9.7
|
|||||||
Capacity
kg/h
|
14085
|
2273
|
11812
|
693
|
|||||||
Running
hours between CIP
|
20
|
20
|
20
|
20
|
|||||||
Capaciity
per day/kg
|
281700
|
45460
|
236240
|
13860
|
|||||||
UF of
acid NF Retentate (60% WPC)
|
UF Feed
|
UF
Retentate
|
UF
Permeate
|
Powder
with 3.5% moisture
|
|||||||
True
Protein %
|
1.65
|
19.06
|
0.06
|
|
|||||||
NPN %
|
0.42
|
0.77
|
0.35
|
|
|||||||
Lactose
%
|
14.66
|
6.71
|
13.78
|
|
|||||||
Acid %
|
0.53
|
0.29
|
0.49
|
|
|||||||
Ash %
|
2.57
|
2.79
|
2.28
|
|
|||||||
Fat %
|
0.16
|
1.85
|
0.01
|
|
|||||||
Total
Solids %
|
19.98
|
31.47
|
16.97
|
96.5
|
|||||||
Protein
/ Total Solids
|
|
63
|
|
|
|||||||
Ash /
Powder
|
|
|
|
8.56
|
|||||||
Capacity
kg/h
|
14085
|
1174
|
14411
|
382
|
|||||||
Running
Hour between CIP
|
20
|
20
|
20
|
20
|
|||||||
Get complete information about dairy plant setup and configuration as per capacity of milk quantity. Engineering fiver provide A to Z information about it. Contact for P&ID, Layout, fabrication drawing and more
Monday, 17 June 2019
NF plant
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